AU2017353264B2

AU2017353264B2 - Process for purification of pyrazolpyridazines

Info

Publication number: AU2017353264B2
Application number: AU2017353264A
Authority: AU
Inventors: Henricus Maria Martinus Bastiaans; Jochen Dietz; Joachim Gebhardt; Birgit GOCKEL; Roland Goetz; Eric KLAUBER; Sebastian Soergel
Original assignee: BASF SE
Current assignee: BASF SE
Priority date: 2016-11-04
Filing date: 2017-10-27
Publication date: 2021-08-05
Anticipated expiration: 2037-10-27
Also published as: MX389871B; PT3535257T; LT3535257T; CN109843875A; MX2019005254A; BR112019009078A2; ZA201903408B; DK3535257T3; US20190308954A1; WO2018083040A1; PL3535257T3; AU2017353264A1; ES2858699T3; BR112019009078B1; SI3535257T1; HRP20210321T1; AR110119A1; EP3535257A1; CY1123846T1; US10961226B2

Abstract

The present invention relates to a process for the purification of pyrazolpyridazines of formula I, wherein the variables are as defined in the specification, by adding HCl to a solution of the pyra- zolpyridazine in an inert solvent under non-aqueos conditions, effecting crystallization of the HCl-salt, isolating the resulting precipitate.

Description

Process for purification of Pyrazolpyridazines

Description

The present invention relates to a process for the purification of pyrazolpyridazines of formulaI 0

2 N N R C)H 3 R CH3 wherein R 1 is H, CH 3 , or C 2H 5 ; and R2 is CH 3 , CH(CH 3) 2, CHFCH 3 , CF(CH 3) 2, CH(CH 3)CF 3 , CHF 2, or cyclopropyl which is substi tuted by halogen or cyano;

by reacting HCI with a solution of the pyrazolpyridazine in an inert solvent, effecting crystalliza tion of the HCI-salt, isolating the resulting precipitate being the HCI salt of formula I compound.

The pyrazolpyridazines of formula I can be obtained from the HCI salt by neutralization by add ing a base to the salt, preferably to a solution of the salt in water, followed by extraction with an organic solvent.

The pyrazolpyridazines of formula I and their insecticidal activity are known from W02012/143317. Although highly efficient manufacturing processes for such compounds are available, the raw product compound of formula I usually contains minor amounts of chemical compounds different from formula I that were created during synthesis as by-products, and hence there is ongoing need for purification of the active compound after synthesis.

It has been found that pure compound of formula I can be obtained from the process as de fined in the outset by isolation of its HCI salt. The by-products and other impurities remain in so lution whereas the HCI salt of formula I compound precipitates from the solution. The HCI salt of formula I compound is a 1:1 salt: one mole of formula I is associated with one mole HCI.

Another use for such process is to separate and collect pyrazolpyridazines of formula I from mother liquors obtained in the manufacturing process. By adding HCI to such mother liquor the HCI salt precipitates and can be separated in high purity. The synthesis of compounds of for mula I is known from the art as referenced above. Mother liquors from the synthesis usually contain 1 to 5 % by weight of formula I compounds and aliphatic and aromatic hydrocarbons as solvents, such as toluene, heptane, cyclohexane, xylenes, chlorobenezens, and alkyl acetates. Accordingly, this process is conducted by introducing HCI into such a solution of pyrazolpyri dazines of formula I and precipitation of the respective formula I compound salt.

Pure means a content of at least 90 %, preferably 95 %, and more preferably 98 % by weight of formula I pyrazolpyridazine salt. The pure salt consists of 90% by weight of formula I com pound and 10 % by weight of HCI. Impurities is counted any organic chemical material different from formula I salt. Purity is measured by HPLC of the free base and by elemental analysis of the salt.

The process for manufacture of the salt is carried out in a solvent wherein the formula I com pound may be dissolved. Non-aqueous conditions are preferred to precipitate the salt from the solution, which means a water content in the solution of not more than 0.5 %, preferably not more than 0.1% water per weight.

Suitable solvents are aliphatic hydrocarbons such as pentane, hexane, cyclohexane, and petrol ether, aromatic hydrocarbons such as toluene, o-, m-, and p-xylene, halogenated hydrocarbons such as methylene chloride, chloroform, and chlorobenzene, ethers such as diethylether, Diiso propylether, tert.-butylmethylether, dioxane, anisole, and tetrahydrofurane (THF), methyl-THF, cyclopentylmethylether, nitrils such as acetonitrile, and propionitrile, ketons such as acetone, methyl ethyl ketone, diethyl ketone, and tert.-butyl methyl ketone, moreover, dimethyl sulphox ide, dimethyl formamide, and dimethylacetamide, preferably aliphatic hydrocarbons, ethers such as dioxane, and aromatic hydrocarbons such as toluene, o-, m-, and p-xylene, particularly tolu ene. It is also possible to use mixtures of the solvents mentioned.

HCI is provided preferably in gaseous form. It is preferably introduced into the reaction mixture by bubbling it continuously through the solvent, wherein the production of the salt shall be per formed, and wherein the formula I compound may already be dissolved. The HCI gas may be added via a dip-tube to make sure the gas is delivered to the solution. In this case, the dip-tube should preferably be fitted with a frit or filter to ensure that solid material does not impede the HCI addition. The HCI gas may be quenched in a scrubber containg a base once it left the reac tor.

Alternatively, compound of formula I compound is dissolved in an organic solvent in a pressure reactor whereafter the reactor can be pressurized with 1.1 to 5 equiv of HCI, and then the reac tion mixture is stirred until completion of the reaction. In this case the HCI gas is led onto the surface of the solution.

Alternatively, a reactor can be pressurized with 1.1 to 5 equiv of HCI, and then the formula I compound is added thereto. Preferably the formula I compound is added being dissolved in a solvent, and the reaction mixture is stirred until completion of the reaction. In this case the HCI gas is led onto the surface of the solution.

Alternatively, the HCI can be dissolved in an organic solvent, for example, dioxane, THF, di ethyl ether or others, to which solution the formula I compound is added. Preferably the formula I compound is added being dissolved in a solvent, and the reaction mixture is stirred until com pletion of the reaction.

The amount of HCI itself is not particularly critical. In general, from 0.7 to 5 mol of HCI are used per mole of compound of formula I used, preferably from 0.8 to 2 mol of HCI per mole of com pound I, more preferably from 0.9 to 1.3 mol of HCI per mole of compound I. The formation of the salt by means of HCI is effected generally at from -10 to 50°C, especially from 5 to 30°C, and at standard pressure or slightly elevated pressure, up to about 10, preferably 5, more pref erably up to 3 bar.

HCI can be used in excess to the formula I compound to maximize the yield of the salt for mation. For economic reasons, in order to minimize the amount of HCI needed, the process is preferably carried out in a closed pressure reactor. HCI gas is introduced preferably above the solution. Ususally 1.05 to 5 mole equivalents HCI to formula I compound are sufficient for a complete crystallization of formula I salt; more preferably 1.05 to 1.5 mole equivalents yield in a complete crystallization. The process is preferably carried out under the HCI pressure that de velops during HCI addition. Preferably the solution is stirred during HCI addition to achieve a homognous HCI concentration in the solution.

For economical and practical reasons, the concentration of formula I compound is usually at least 10 % and up to a saturated solution, the concentration in the saturated solution depends on the nature of the solvent and the temperature. For practical reasons a concentration from 15 to 25 % by weight is preferred.

The process is carried out at temperatures of from -20°C to 100°C, preferably from 0°C to 40°C. It is preferably conducted in an inert solvent such as toluene, tetrahydrofurane (THF), or dioxane, in the presence of HCI in an amount of at least 1.0 mol equivalent.

The formula I compound can be used in form of its HCI salt, e.g. in agricultural formulations. If the formula I compound is being used as free base, the salt will be neutralized by adding about one mole of a base to the salt.

Suitable bases are, in general, inorganic compounds, such as alkali metal and alkaline earth metal hydroxides, such as lithium hydroxide, sodium hydroxide, potassium hydroxide and cal cium hydroxide, alkali metal and alkaline earth metal oxides, such as lithium oxide, sodium ox ide, calcium oxide, and magnesium oxide, alkali metal and alkaline earth metal hydrides, such as lithium hydride, sodium hydride, potassium hydride and calcium hydride, alkali metal and al kaline earth metal carbonates, such as lithium carbonate, potassium carbonate and calcium car bonate, and also alkali metal bicarbonates, such as sodium bicarbonate, moreover, organic ba ses, for example tertiary amines, such as trimethylamine, triethylamine, triisopropylethylamine and N-methylpiperidine, pyridine, substituted pyridines, such as collidine, lutidine and 4-dime thylaminopyridine, and also bicyclic amines. Particular preference is given to K 2 CO 3 , NaOH, or triethylamine. The bases are generally employed in equimolar amounts, in excess or, if appro priate, as solvent.

If desired, it may be advantageous to remove the salt formed from HCI and formula I in the course of the neutralization before the further processing of formula I compounds, for example, by means of filtration methods. With regard to the filtration of the salt, a particularly advanta geous procedure is that in the presence of a small water content (for example when the HCI gas is introduced). This generally gave rise to significantly shorter filtration times, which may be highly advantageous for the procedure on the industrial scale.

The process is particularly applicable to a compound selected from compounds 1-1 to1-3 which are: 1-(1,2-dimethylpropyl)-N-ethyl-5-methyl-N-pyridazin-4-yl-pyrazole-4-carboxamide (1-1), 1-[1 (1-cyanocyclopropyl)ethyl]-N-ethyl-5-methyl-N-pyridazin-4-yl-pyrazole-4-carboxamide (1-2), and N-ethyl-i-(2-fluoro-1-methyl-propyl)-5-methyl-N-pyridazin-4-yl-pyrazole-4-carboxamide (1-3).

The HCI salt can be directly used in any acidic agricultural formulations of the pyrazolpyri dazine compound.

The invention also relates to agrochemical compositions comprising an auxiliary and at least one salt compound of the present invention or a mixture thereof.

An agrochemical composition comprises a pesticidally effective amount of a salt compound of the present invention or a mixture thereof. The term "pesticidally effective amount" is defined below. The HCI salt compounds of formula I or the mixtures thereof can be converted into customary types of agro-chemical compositions, e. g. solutions, emulsions, suspensions, dusts, powders, pastes, granules, pressings, capsules, and mixtures thereof. Examples for composition types are suspensions (e.g. SC, OD, FS), emulsifiable concentrates (e.g. EC), emulsions (e.g. EW, EO, ES, ME), capsules (e.g. CS, ZC), pastes, pastilles, wettable powders or dusts (e.g. WP, SP, WS, DP, DS), pressings (e.g. BR, TB, DT), granules (e.g. WG, SG, GR, FG, GG, MG), in secticidal articles (e.g. LN), as well as gel formulations for the treatment of plant propagation materials such as seeds (e.g. GF). These and further compositions types are defined in the "Catalogue of pesticide formulation types and international coding system", Technical Mono graph No. 2, 6th Ed. May 2008, CropLife International. Preferred formulation types are: SL, SG, WP, OD, tablets, gel baits, CS (water in oil capsules), and Water in oil emulsions. The compositions are prepared in a known manner, such as described by Mollet and Grube mann, Formulation technology, Wiley VCH, Weinheim, 2001; or Knowles, New developments in crop protection product formulation, Agrow Reports DS243, T&F Informa, London, 2005. Examples for suitable auxiliaries are solvents, liquid carriers, solid carriers or fillers, surfac tants, dispersants, emulsifiers, wetters, adjuvants, solubilizers, penetration enhancers, protec tive colloids, adhesion agents, thickeners, humectants, repellents, attractants, feeding stimu lants, compatibilizers, bactericides, anti-freezing agents, anti-foaming agents, colorants, tackifi ers and binders. Suitable solvents and liquid carriers are water and organic solvents, such as mineral oil frac tions of medium to high boiling point, e.g. kerosene, diesel oil; oils of vegetable or animal origin; aliphatic, cyclic and aromatic hydrocarbons, e. g. toluene, paraffin, tetrahydronaphthalene, al kylated naphthalenes; alcohols, e.g. ethanol, propanol, butanol, benzylalcohol, cyclohexanol; glycols; DMSO; ketones, e.g. cyclohexanone; esters, e.g. lactates, carbonates, fatty acid esters, gamma-butyrolactone; fatty acids; phosphonates; amines; amides, e.g. N-methylpyrrolidone, fatty acid dimethylamides; and mixtures thereof.

Suitable solid carriers or fillers are mineral earths, e.g. silicates, silica gels, talc, kaolins, lime stone, lime, chalk, clays, dolomite, diatomaceous earth, bentonite, calcium sulfate, magnesium sulfate, magnesium oxide; polysaccharide powders, e.g. cellulose, starch; fertilizers, e.g. ammo nium sulfate, ammonium phosphate, ammonium nitrate, ureas; products of vegetable origin, e.g. cereal meal, tree bark meal, wood meal, nutshell meal, and mixtures thereof. Suitable surfactants are surface-active compounds, such as anionic, cationic, nonionic and amphoteric surfactants, block polymers, polyelectrolytes, and mixtures thereof. Such surfactants can be used as emusifier, dispersant, solubilizer, wetter, penetration enhancer, protective col loid, or adjuvant. Examples of surfactants are listed in McCutcheon's, Vol.1: Emulsifiers & De tergents, McCutcheon's Directories, Glen Rock, USA, 2008 (International Ed. or North American Ed.). Suitable anionic surfactants are alkali, alkaline earth or ammonium salts of sulfonates, sul fates, phosphates, carboxylates, and mixtures thereof. Examples of sulfonates are alkylaryl-sul fonates, diphenylsulfonates, alpha-olefin sulfonates, lignine sulfonates, sulfonates of fatty acids and oils, sulfonates of ethoxylated alkylphenols, sulfonates of alkoxylated arylphenols, sulfo nates of condensed naphthalenes, sulfonates of dodecyl- and tridecylbenzenes, sulfonates of naphthalenes and alkylhnaphthalenes, sulfosuccinates or sulfosuccinamates. Examples of sul fates are sulfates of fatty acids and oils, of ethoxylated alkylphenols, of alcohols, of ethox-ylated alcohols, or of fatty acid esters. Examples of phosphates are phosphate esters. Exam-ples of carboxylates are alkyl carboxylates, and carboxylated alcohol or alkylphenol eth-oxylates. Suitable nonionic surfactants are alkoxylates, N-subsituted fatty acid amides, amine oxides, esters, sugar-based surfactants, polymeric surfactants, and mixtures thereof. Examples of alkoxylates are compounds such as alcohols, alkylphenols, amines, amides, arylphenols, fatty acids or fatty acid esters which have been alkoxylated with 1 to 50 equivalents. Ethylene oxide and/or propylene oxide may be employed for the alkoxylation, preferably ethylene oxide. Exam ples of N-subsititued fatty acid amides are fatty acid glucamides or fatty acid alkanolamides. Ex amples of esters are fatty acid esters, glycerol esters or monoglycerides. Examples of sugar based surfactants are sorbitans, ethoxylated sorbitans, sucrose and glucose esters or alkylpoly glucosides. Examples of polymeric surfactants are homo- or copolymers of vinylpyrrolidone, vi nylalcohols, or vinylacetate. Suitable cationic surfactants are quaternary surfactants, for example quaternary ammonium compounds with one or two hydrophobic groups, or salts of long-chain primary amines. Suitable amphoteric surfactants are alkylbetains and imidazolines. Suitable block polymers are block pol ymers of the A-B or A-B-A type comprising blocks of polyethylene oxide and polypropylene ox ide, or of the A-B-C type comprising alkanol, polyethylene oxide and polypropylene oxide. Suita ble polyelectrolytes are polyacids or polybases. Examples of polyacids are alkali salts of poly acrylic acid or polyacid comb polymers. Examples of polybases are polyvinylamines or polyeth yleneamines. Suitable adjuvants are compounds, which have a neglectable or even no pesticidal activity themselves, and which improve the biological performance of the compounds of the present in vention on the target. Examples are surfactants, mineral or vegetable oils, and other auxilaries. Further examples are listed by Knowles, Adjuvants and additives, Agrow Reports DS256, T&F Informa UK, 2006, chapter 5.

Suitable thickeners are polysaccharides (e.g. xanthan gum, carboxymethylcellulose), anor ganic clays (organically modified or unmodified), polycarboxylates, and silicates. Suitable bactericides are bronopol and isothiazolinone derivatives such as alkylisothiazoli nones and benzisothiazolinones. Suitable anti-freezing agents are ethylene glycol, propylene glycol, urea and glycerin. Suitable anti-foaming agents are silicones, long chain alcohols, and salts of fatty acids. Suitable colorants (e.g. in red, blue, or green) are pigments of low water solubility and water soluble dyes. Examples are inorganic colorants (e.g. iron oxide, titan oxide, iron hexacyanofer rate) and organic colorants (e.g. alizarin-, azo- and phthalocyanine colorants). Suitable tackifiers or binders are polyvinylpyrrolidons, polyvinylacetates, polyvinyl alcohols, polyacrylates, biological or synthetic waxes, and cellulose ethers. Examples for composition types of the HCI salt (which is referred to "compound I" in the follow ing examples) and their preparation are: i) Water-soluble concentrates (SL, LS) 10-60 wt% of a compound I according to the invention and 5-15 wt% wetting agent (e.g. alcohol alkoxylates) are dissolved in water and/or in a water-soluble solvent (e.g. alcohols) up to 100 wt%. The active substance dissolves upon dilution with water. ii) Dispersible concentrates (DC) 5-25 wt% of a compound I according to the invention and 1-10 wt% dispersant (e. g. polyvi nylpyrrolidone) are dissolved in up to 100 wt% organic solvent (e.g. cyclohexanone). Dilution with water gives a dispersion. iii) Emulsifiable concentrates (EC) 15-70 wt% of a compound I according to the invention and 5-10 wt% emulsifiers (e.g. calcium dodecylbenzenesulfonate and castor oil ethoxylate) are dissolved in up to 100 wt% water-insol uble organic solvent (e.g. aromatic hydrocarbon). Dilution with water gives an emulsion. iv) Emulsions (EW, EO, ES) 5-40 wt% of a compound I according to the invention and 1-10 wt% emulsifiers (e.g. calcium do decylbenzenesulfonate and castor oil ethoxylate) are dissolved in 20-40 wt% water-insoluble or ganic solvent (e.g. aromatic hydrocarbon). This mixture is introduced into up to 100 wt% water by means of an emulsifying machine and made into a homogeneous emulsion. Dilution with wa ter gives an emulsion. v) Suspensions (SC, OD, FS) In an agitated ball mill, 20-60 wt% of a compound I according to the invention are comminuted with addition of 2-10 wt% dispersants and wetting agents (e.g. sodium lignosulfonate and alco hol ethoxylate), 0,1-2 wt% thickener (e.g. xanthan gum) and up to 100 wt% water to give a fine active substance suspension. Dilution with water gives a stable suspension of the active sub stance. For FS type composition up to 40 wt% binder (e.g. polyvinylalcohol) is added. vi) Water-dispersible granules and water-soluble granules (WG, SG) 50-80 wt% of a compound I according to the invention are ground finely with addition of up to 100 wt% dispersants and wetting agents (e.g. sodium lignosulfonate and alcohol ethoxylate) and prepared as water-dispersible or water-soluble granules by means of technical appliances (e. g. extrusion, spray tower, fluidized bed). Dilution with water gives a stable dispersion or solu tion of the active substance.

vii) Water-dispersible powders and water-soluble powders (WP, SP, WS) 50-80 wt% of a compound I according to the invention are ground in a rotor-stator mill with ad dition of 1-5 wt% dispersants (e.g. sodium lignosulfonate), 1-3 wt% wetting agents (e.g. alcohol ethoxylate) and up to 100 wt% solid carrier, e.g. silica gel. Dilution with water gives a stable dis persion or solution of the active substance. viii) Gel (GW, GF) In an agitated ball mill, 5-25 wt% of a compound I according to the invention are comminuted with addition of 3-10 wt% dispersants (e.g. sodium lignosulfonate), 1-5 wt% thickener (e.g. car boxymethylcellulose) and up to 100 wt% water to give a fine suspension of the active sub stance. Dilution with water gives a stable suspension of the active substance. ix) Microemulsion (ME) 5-20 wt% of a compound I according to the invention are added to 5-30 wt% organic solvent blend (e.g. fatty acid dimethylamide and cyclohexanone), 10-25 wt% surfactant blend (e.g. alko hol ethoxylate and arylphenol ethoxylate), and water up to 100 %. This mixture is stirred for 1 h to produce spontaneously a thermodynamically stable microemulsion. x) Microcapsules (CS) An oil phase comprising 5-50 wt% of a compound I according to the invention, 0-40 wt% water insoluble organic solvent (e.g. aromatic hydrocarbon), 2-15 wt% acrylic monomers (e.g. methyl methacrylate, methacrylic acid and a di- or triacrylate) are dispersed into an aqueous solution of a protective colloid (e.g. polyvinyl alcohol). Radical polymerization initiated by a radical initiator results in the formation of poly(meth)acrylate microcapsules. xi) Dustable powders (DP, DS) 1-10 wt% of a compound I according to the invention are ground finely and mixed intimately with up to 100 wt% solid carrier, e.g. finely divided kaolin. xii) Granules (GR, FG) 0.5-30 wt% of a compound I according to the invention is ground finely and associated with up to 100 wt% solid carrier (e.g. silicate). Granulation is achieved by extrusion, spray-drying or the fluidized bed. The compositions types i) to xi) may optionally comprise further auxiliaries, such as 0.1-1 wt% bactericides, 5-15 wt% anti-freezing agents, 0.1-1 wt% anti-foaming agents, and 0.1-1 wt% col orants. The agrochemical compositions generally comprise between 0.01 and 95%, preferably be tween 0.1 and 90%, and most preferably between 0.5 and 75%, by weight of active sub-stance. The active substances are employed in a purity of from 90% to 100%, preferably from 95% to 100% (according to NMR spectrum). Various types of oils, wetters, adjuvants, fertilizer, or micronutrients, and other pesticides (e.g. herbicides, insecticides, fungicides, growth regulators, safeners) may be added to the active substances or the compositions comprising them as premix or, if appropriate not until immedi ately prior to use (tank mix). These agents can be admixed with the compositions according to the invention in a weight ratio of 1:100 to 100:1, preferably 1:10 to 10:1. The user applies the composition according to the invention usually from a predosage de-vice, a knapsack sprayer, a spray tank, a spray plane, or an irrigation system. Usually, the agrochem ical composition is made up with water, buffer, and/or further auxiliaries to the desired applica tion concentration and the ready-to-use spray liquor or the agrochemical composition according to the invention is thus obtained. Usually, 20 to 2000 liters, preferably 50 to 400 liters, of the ready-to-use spray liquor are applied per hectare of agricultural useful area. According to one embodiment, individual components of the composition according to the in vention such as parts of a kit or parts of a binary or ternary mixture may be mixed by the user himself in a spray tank and further auxiliaries may be added, if appropriate. In a further embodiment, either individual components of the composition according to the in vention or partially premixed components, e. g. components comprising compounds of the pre sent invention and/or mixing partners as defined above, may be mixed by the user in a spray tank and further auxiliaries and additives may be added, if appropriate. In a further embodiment, either individual components of the composition according to the in vention or partially premixed components, e. g. components comprising compounds of the pre sent invention and/or mixing partners as defined above, can be applied jointly (e.g. after tank mix) or consecutively.

Examples

The products shown below were characterized by NMR spectroscopy or by elemental analysis.

Dry toluene contains up to 500 ppm water.

Manufacture of 1-(1,2-dimethylpropyl)-N-ethyl-5-methyl-N-pyridazin-4-yl-pyrazole-4-carbox amide x 1 HCI salt

Example 1: A solution of 7.25 g of 1-(1,2-dimethylpropyl)-N-ethyl-5-methyl-N-pyridazin-4-yl-pyrazole-4-car boxamide (99% purity) in 28 g dry toluene was added to a nitrogen filled pressure reactor and stir at 25°C. HCI gas was slowly bubbled through for 1 h producing a thick slurry. The solution is allowed to stir for an additional hour at 20 to 25°C. The reactor is flushed with nitrogen and the slurry is filtered through nutsche. The salt is washed with toluene, then dried at 50 °C in a vac uum oven. Yield: 8.00 g of the title compound salt

Elemental analysis: calculated for C 1 H 2 2 N5 0C) C 56.9% (56.5%) H 7.2% (7.1%) N 20.6% (21.3%) o 5.0% (4.7%) Cl 10.2% (10.4%)

Example 2: A solution of 43,7 g of 1-(1,2-dimethylpropyl)-N-ethyl-5-methyl-N-pyridazin-4-yl-pyrazole-4-car boxamide (93,8% purity) in 215 g dry toluene was added to a nitrogen filled pressure reactor and stir at 25°C. The pressure reactor is charged with HCI gas (7,4 g (1.5 equiv)). The solution is allowed to stir for 2 hours at 20 to 25 C producing a thick slurry. The reactor is depres surized, flushed with nitrogen and the slurry is filtered through nutsche. The salt is washed with toluene, then dried at 50 C in a vacuum oven. 0

Yield: 28.0 g of the title compound salt

Example 3: Neutralization 2.00 g 1-(1,2-dimethylpropyl)-N-ethyl-5-methyl-N-pyridazin-1-ium-4-yl-pyrazole-4-carbox amide chloride were dissolved in 40 g water. The pH of the solution was adjusted from pH 1.6 to pH 5 with 2N NaOH. The solution was then extracted twice with 30 ml of toluene. Tol uene was removed yielding 2.1 g of compound I-1 as an oil which contained 83.4% of com pound I-1 and 16% toluene. The aqueous layer contained less than 0.1% of compound I-1.

It is to be understood that, if any prior art publication is referred to herein, such reference does not constitute an admission that the publication forms a part of the common general knowledge in the art, in Australia or any other country.

In the claims which follow and in the preceding description of the invention, except where the context requires otherwise due to express language or necessary implication, the word "comprise" or variations such as "comprises" or "comprising" is used in an inclusive sense, i.e. to specify the presence of the stated features but not to preclude the presence or addi tion of further features in various embodiments of the invention.

Claims

1. A process for the purification of pyrazolpyridazines of formulaI 0

2 N CH 3 OH 3 wherein R' is H, CH 3 , or C 2 H 5 ; and R2 C 1-C 4-alkyl, C -C 1 4-haloalkyl, cyclopropyl which is substituted by halogen or cy ano; by adding HCI to a solution of the pyrazolpyridazine in an inert solvent under non aqueos conditions, effecting crystallization of the HCI-salt of the formula I compound, and isolating the resulting precipitate.

2. A process according to claim 1, wherein the solvent is selected from aliphatic solvents.

3. A process according to claim 1, wherein the solvent is selected from toluene, o-, m-, and p-xylene.

4. A process according to any one of claims 1 to 3, wherein the concentration of formula I compound in the solvent is from 15 to 25 %by weight.

5. A process according to any one of claims 1 to 4, further comprising neutralization of the HCI-salt which is effected with triethylamine, K2 CO 3 , or NaOH.

6. A process according to any one of claims 1 to 5, wherein R 2 in formula I is selected from CH 3 , CH(CH 3) 2, CHFCH 3, CF(CH 3) 2, CH(CH 3)CF 3, CHF 2, and 1-CN-C 3 H 4 .

7. A process according to any one of claim 1 to 6, wherein the formula I compound is se lected from compounds 1-1 to1-3 which are: 1-(1,2-dimethylpropyl)-N-ethyl-5-methyl N-pyridazin-4-yl-pyrazole-4-carboxamide (I-1), 1-[1-(1-cyanocyclopropyl)ethyll-N ethyl-5-methyl-N-pyridazin-4-yl-pyrazole-4-carboxamide (1-2), and N-ethyl-1-(2 fluoro-1-methyl-propyl)-5-methyl-N-pyridazin-4-yl-pyrazole-4-carboxamide (1-3).

8. The 1:1 HCI salt of 1-(1,2-dimethylpropyl)-N-ethyl-5-methyl-N-pyridazin-4-yl-pyra zole-4-carboxamide.

9. An agricultural composition comprising the salt compound as defined in claim 8 and at least one inert liquid and/or solid acceptable carrier and, if desired, at least one sur factant.